Method for scrubbing exhaust gas from CO
A method of exhaust gas scrubbing includes providing recycled concrete fines as a waste material rich in carbonatable Ca and/or Mg phases and with d 90 ≤1000 μm and a Rosin-Rammler slope n from 0.6 to 1.4 , injecting the waste material into an exhaust gas stream containing CO 2 and/or SO x for reaction with CO 2 and/or SO x at a relative humidity of 50 to 100 Vol.-% and a temperature from 40 to 130° C. in an amount of dry waste material ranging from 5 to 30 kg/m 3 , withdrawing a partly carbonated and/or sulphurized waste material and purified exhaust gas, and recycling a part of the partly carbonated and sulphurized waste material while the remainder is discharged, as well as use of a waste material slurry for exhaust gas cleaning of CO 2 and/or SO x .
1. A method for scrubbing an exhaust gas from CO 2 and SO x with x from 1 to 3, comprising the steps:
providing recycled concrete fines with d 90 ≤1000 μm and a Rosin-Rammler slope n from 0.6 to 1.4 in dry form or as a slurry,
injecting the recycled concrete fines into the exhaust gas for reaction with CO 2 and SO x to provide in the exhaust gas stream an amount of dry recycled concrete fines ranging from 5 to 30 kg/m 3 , and adjustung a relative humidity from 50 to 100% and a temperature from 40 to 130° C.,
withdrawing partly carbonated and/or sulphurized recycled concrete fines and cleaned exhaust gas
recycling a part of the partly carbonated and sulphurized recycled concrete fines while the remainder is discharged.
2. The method according to claim 1 , wherein the recycled concrete fines are from recycling and reuse of used concrete.
3. The method according to claim 1 , wherein the recycled concrete fines are added as a slurry containing from 4 to 28% by weight solids and in an amount from 20 to 50 l/m 3 .
4. The method according to claim 3 , wherein the temperature during reaction of the recycled concrete fines with CO 2 and SO x in the exhaust gas is adjusted to from 55 to 75° C. for injection of the recycled concrete fines as a slurry at a relative humidity of 100%.
5. The method according to claim 1 , wherein at least 12.5 wt.-% of the recycled concrete fines calculated as oxides is CaO and MgO and at least 80 wt.-% of the CaO and MgO are in carbonatable phases before carbonation.
6. The method according to claim 5 , wherein at least 20 wt.-% of the recycled concrete fines calculated as oxides is CaO and MgO and at least 85 wt.-% of the CaO and MgO are in carbonatable phases.
7. The method according to claim 5 , wherein at least 30 wt.-% of the recycled concrete fines calculated as oxides is CaO and MgO and at least 90 wt.-% of the CaO and MgO are in carbonatable phases.
8. The method according to claim 1 , additionally comprising mechanical pretreatment of the recycled concrete fines.
9. The method according to claim 1 , wherein the recycled concrete fines have a particle size distribution having a d 90 ≤500 μm and/or a Rosin-Rammler slope n from 0.7 to 1.2.
10. The method according to claim 9 , wherein at least 20 wt.-% of the recycled concrete fines calculated as oxides is CaO and MgO and at least 85 wt.-% of the CaO and MgO are in carbonatable phases.
11. The method according to claim 10 , wherein the recycled concrete fines are added as a slurry containing from 4 to 28% by weight solids and in an amount from 20 to 50 l/m 3 .
12. The method according to claim 11 , wherein the temperature during reaction of the recycled concrete fines with CO 2 and SO x in the exhaust gas is adjusted to from 55 to 75° C. for injection of the recycled concrete fines as a slurry at a relative humidity of 100%.
13. The method according to claim 11 , wherein the weight ratio between recycled and discharged recycled concrete fines ranges from 6000 to 200.
14. The method according to claim 10 , wherein the temperature during reaction of the recycled concrete fines with CO 2 and SO x in the exhaust gas is adjusted to from 55 to 85° C. for injection of the recycled concrete fines as dry material with or without injection of water and/or slurry at a relative humidity from 50 to 95%.
15. The method according to claim 1 , wherein the exhaust gas is taken from a plant burning fuel to generate heat for a material or energy production process.
16. The method according to claim 15 , wherein the exhaust gas is taken from a coal fired power plant, a ceramics manufacturing plant, the magnesia industry, a lime kiln, or a cement plant.
17. The method according to claim 16 , wherein before or after cleaning the exhaust gas is further subjected to one or more of:
dust removal,
gas cooling,
gas conditioning,
heat recovery,
and/or the cleaned exhaust gas is used for drying of wet materials.
18. The method according to claim 17 , wherein the weight ratio between recycled and discharged recycled concrete fines ranges from 6000 to 200.
19. The method according to claim 1 , wherein sulfur is removed from or diminished in the exhaust gas prior to scrubbing with the recycled concrete fines.
20. The method according to claim 1 , wherein the temperature during reaction of the recycled concrete fines with CO 2 and SO x in the exhaust gas is adjusted to from 55 to 85° C. for injection of the recycled concrete fines as dry material with or without injection of water and/or slurry at a relative humidity from 50 to 95%.
21. The method according to claim 1 , wherein the weight ratio between recycled and discharged recycled concrete fines ranges from 10000 to 100.
22. The method according to claim 21 , wherein the weight ratio between recycled and discharged recycled concrete fines ranges from 6000 to 200.
23. The method according to claim 1 , wherein before or after cleaning the exhaust gas is further subjected to one or more of:
dust removal,
gas cooling,
gas conditioning,
heat recovery,
and/or the cleaned exhaust gas is used for drying of wet materials.